JPH02214521A - Controller for injection amount of gaseous ammonia - Google Patents

Controller for injection amount of gaseous ammonia

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Publication number
JPH02214521A
JPH02214521A JP1035023A JP3502389A JPH02214521A JP H02214521 A JPH02214521 A JP H02214521A JP 1035023 A JP1035023 A JP 1035023A JP 3502389 A JP3502389 A JP 3502389A JP H02214521 A JPH02214521 A JP H02214521A
Authority
JP
Japan
Prior art keywords
signal
ammonia gas
set value
amount
outputted
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP1035023A
Other languages
Japanese (ja)
Other versions
JP2695654B2 (en
Inventor
Takao Yanagida
柳田 喬夫
Tsuguaki Doi
土井 継昭
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1035023A priority Critical patent/JP2695654B2/en
Publication of JPH02214521A publication Critical patent/JPH02214521A/en
Application granted granted Critical
Publication of JP2695654B2 publication Critical patent/JP2695654B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To inject an appropriate amt. of gaseous ammonia by providing an integral controller for inputting a deviation signal from a comparator for inputting an excess gaseous ammonia concn. set value signal and an ammonia concn. signal and for outputting a conversion rate correction signal to be inputted to a computing element. CONSTITUTION:The computing element 6 for correcting the reactant gaseous ammonia amt. signal 1 by a set value signal 120 for the sulfur content in fuel is provided, an ammonia injection amt. signal 20 is outputted. An excess gaseous ammonia concn. set value 3 outputted from a gaseous ammonia concn. setter 113 and a gaseous ammonia concn. signal 2 outputted from a gaseous ammonia densitometer 111 are inputted to the comparator 115. A deviation signal 4 outputted from the comparator 115 is inputted to a high/low signal detector 5, and the deviation signal beyond the upper or lower set value is selected. The signal outputted from the selector 5 is inputted to the integral controller 7, the conversion rate correction signal 8 proportional to the time when the deviation signal 4 is beyond the upper or lower set value is outputted, and the signal 8 is inputted to the computing element 6.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ボイラに用いる電気集塵器(以下EPという
)等の脱硫に用いるアンモニアガス注入量の制御装置に
関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a control device for controlling the amount of ammonia gas injected for desulfurization of an electrostatic precipitator (hereinafter referred to as EP) used in a boiler.

〔従来の技術〕[Conventional technology]

IPの入口側煙道にアンモニアガスを注入して脱硫を行
う装置においては、第2図に示すようにEP108の入
口側煙道107に注入管を介してアンモニアガスを注入
して脱硫処理を行い浄化ガスをEP出口側煙道109を
経て排出させている。
In a device that performs desulfurization by injecting ammonia gas into the inlet flue of an IP, desulfurization is performed by injecting ammonia gas into the inlet flue 107 of the EP 108 through an injection pipe, as shown in Figure 2. The purified gas is discharged through a flue 109 on the EP outlet side.

上記アンモニアガスの注入量制御のための従来の制御装
置には、昭和62年出願公開第171733号(昭和6
1年特許願第12118号)によシ提案された第2図及
び第3図に示すものがある。
The conventional control device for controlling the amount of ammonia gas injected is disclosed in Application Publication No. 171733 of 1988 (Showa 6).
There is a method shown in FIGS. 2 and 3, which was proposed by U.S. Pat.

即ち、EP108C)入口煙道107に注入されるアン
モニアガス量は、燃料流量信号101、燃料中の硫黄分
設定値信号120.EP出ロアンモニア濃度設定器11
3の出力信号及びEP108の出口煙道109の排ガス
中のアンモニアガス濃度を検出するアンモニアガス濃度
計111の出力信号を入力し九演算回路102の出力信
号とアンモニアガス注入管106J’C設置されたアン
モニアガス注入量検出器103の出力信号とを調節器1
04で比較し、その偏差信号によシアンモニアガス注入
管106に設置された調節弁105を開閉して、増減さ
れるものである。
That is, EP108C) The amount of ammonia gas injected into the inlet flue 107 is determined by the fuel flow rate signal 101, the sulfur content set value signal 120. EP output ammonia concentration setting device 11
3 and the output signal of the ammonia gas concentration meter 111 that detects the ammonia gas concentration in the exhaust gas at the outlet flue 109 of the EP 108 are input, and the output signal of the 9 arithmetic circuit 102 and the ammonia gas injection pipe 106J'C are installed. The output signal of the ammonia gas injection amount detector 103 and the regulator 1
04, and the control valve 105 installed in the cyanmonia gas injection pipe 106 is opened and closed according to the deviation signal to increase or decrease the amount.

上記演算回路102においては、燃料流量信号101を
入力した反応用アンモニアガス量演算回路112VCて
反応用アンモニアガス量が求められ、同反応用アンモニ
アガス量は補正回路に入力され燃料中の硫黄分によって
補正された反応用アンモニアガス量が求められる。また
上記燃料流量信号101は余剰用アンモニアガス量演算
回路114に入力されて余剰用アンモニアガス量が求め
られ、同余剰用アンモニアガス量はEP108出口に残
存する余剰用アンモニアガス濃度の設定値を出力する余
剰アンモニアガス濃度設定器113からの信号を入力す
る補正回路によシ補正され、補正された余剰用アンモニ
アガス量が求められる。上記補正された反応用アンモニ
アガス量には、上記補正された余剰用アンモニアガス量
が余剰用アンモニアガス加算器117にて加算され、更
に、余剰用アンモニアガス濃度設定器113が出力し九
設定値とアンモニアガス濃度計111が出力した実測値
より比較器115が出力した余剰用アンモニアガス量補
正信号によってサンプル制御回路116にて補正が行わ
れ、アンモニアガス注入量110が出力される。
In the arithmetic circuit 102, the amount of ammonia gas for reaction is determined by a reaction ammonia gas amount calculation circuit 112VC which receives the fuel flow rate signal 101, and the amount of ammonia gas for reaction is input to a correction circuit and is determined by the sulfur content in the fuel. The corrected reaction ammonia gas amount is determined. Further, the fuel flow rate signal 101 is input to the surplus ammonia gas amount calculation circuit 114 to determine the surplus ammonia gas amount, and the surplus ammonia gas amount outputs the set value of the surplus ammonia gas concentration remaining at the outlet of the EP 108. A correction circuit inputs a signal from the surplus ammonia gas concentration setting device 113, and the corrected surplus ammonia gas amount is determined. The above corrected surplus ammonia gas amount is added to the above corrected reaction ammonia gas amount by the surplus ammonia gas adder 117, and the surplus ammonia gas concentration setting device 113 outputs a nine set value. Based on the actual measurement value outputted by the ammonia gas concentration meter 111, the sample control circuit 116 performs correction based on the surplus ammonia gas amount correction signal outputted by the comparator 115, and the ammonia gas injection amount 110 is output.

上記灰石用アンモニアガスは、燃料中に含まれる硫黄分
と次の反応式で示す反応を行い、硫酸アンモニウム(N
 H4) t S Oaを生成し、同硫酸アンモニウム
(NH4)鵞SO,はEP 108によって除去される
The above ammonia gas for graystone undergoes a reaction with the sulfur content contained in the fuel as shown in the following reaction formula, and is produced by ammonium sulfate (N
Ammonium sulfate (NH4) SO, is removed by EP 108.

S+0.→Sow 280象+0!→2SOs SOs+HxO→H,5o4 N Hs 十He S O4→NH4H3O4NHaH
8Oa+NHs→(NH4)*SOa上記反応用アンモ
ニアガス量は、上記反応式をもとに演算回路102内に
て演算される。
S+0. →Sow 280 elephants +0! →2SOs SOs+HxO→H,5o4 N Hs 10He SO4→NH4H3O4NHaH
8Oa+NHs→(NH4)*SOa The above reaction ammonia gas amount is calculated in the calculation circuit 102 based on the above reaction formula.

量を決定する理由は、アンモニアガスが不足し九場合に
は次式の反応が右に進み (NH4)*SO4二NHs + N H4H804酸
性硫安NHaH8O4を生成してEPに悪影響を及はす
九めである。
The reason for determining the amount is that if there is a shortage of ammonia gas, the reaction of the following formula will proceed to the right (NH4)*SO42NHs + N H4H804 and produce acidic ammonium sulfate NHaH8O4, which will have a negative impact on EP. be.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

従来の装置においては、アンモニアガス濃度針の応答速
度が遅い(約10〜40分)ため、通常の比例積分微分
制御では適量のアンモニアガスを注入することができな
かつ九。
In conventional devices, the response speed of the ammonia gas concentration needle is slow (approximately 10 to 40 minutes), making it impossible to inject an appropriate amount of ammonia gas using normal proportional-integral-derivative control.

まえ、硫黄分の燃焼によって発生するボイラ排ガス中に
含まれるSonの濃度変化には、経時的にゆるやかに増
大する部分(年間100チ程度増加)とボイラの運転状
態や空気過剰率や温度等によって急激に変化する部分が
あるが、従来の装置ではこれらに十分対応することがで
きなかつ九。
First, the concentration of Son contained in boiler exhaust gas generated by combustion of sulfur content changes partly due to a gradual increase over time (approximately 100 cm increase per year) and partly due to boiler operating conditions, excess air ratio, temperature, etc. There are parts that change rapidly, and conventional equipment cannot adequately respond to these changes.

上記Son濃度のゆるやかな増大は、ボイラの使用時間
に伴ってボイラ内に蓄積される重金属が増加し、これが
S01をSOlに転化させる触媒として作用するためで
ある。
The reason for the gradual increase in the Son concentration is that heavy metals accumulated in the boiler increase as the boiler is used, and this acts as a catalyst to convert SO1 to SO1.

本発明は、上記の課題を解決し、常時適量のアンモニア
ガスを注入し、余剰アンモニアガス量を最小限に抑え、
ランニングコストが低減できる装置を提供しようとする
ものである。
The present invention solves the above problems, always injects an appropriate amount of ammonia gas, minimizes the amount of surplus ammonia gas,
The aim is to provide a device that can reduce running costs.

(a題を解決するための手段〕 本発明の制御装置は、反応用アンモニアガス量信号を燃
料中の硫黄分設定値信号によって補正する演算器を備え
アンモニア注入量信号を出力する制御装置において、ア
ンモニアガス濃度設定器が出力する余剰アンモニアガス
濃度設定値信号とアンモニアガス濃度計が出力するアン
モニアガス濃度信号を入力する比較器、同比較器が出力
する偏差信号を入力し上限及び下限設定値を越えた偏差
信号を選択する高低信号選択器、同高低信号選択器が出
力した信号を入力し上記偏差信号が上限及び下限設定値
を越えた時間に比例した転化率補正信号を出力し同信号
を上記演算器に入力させる積分調節器を備えたことを特
徴としている。
(Means for Solving Problem a) The control device of the present invention is a control device that outputs an ammonia injection amount signal and includes a computing unit that corrects a reaction ammonia gas amount signal using a sulfur content set value signal in the fuel. A comparator that inputs the surplus ammonia gas concentration setting value signal output from the ammonia gas concentration setting device and the ammonia gas concentration signal output from the ammonia gas concentration meter, and inputs the deviation signal output from the comparator to set the upper and lower limit set values. A high/low signal selector selects the exceeded deviation signal, inputs the signal output by the same high/low signal selector, outputs a conversion rate correction signal proportional to the time when the deviation signal exceeds the upper and lower limit set values, and outputs the same signal. The present invention is characterized in that it includes an integral regulator that inputs input to the arithmetic unit.

〔作用〕[Effect]

上記において、アンモニアガス濃度設定器より余剰アン
モニアガス濃度設定値信号を入力し、アンモニアガス濃
度計よシアンモニアガス濃度信号を入力した比較器は、
偏差信号を出力する。
In the above, the comparator inputs the surplus ammonia gas concentration setting value signal from the ammonia gas concentration setting device and inputs the cyanmonia gas concentration signal from the ammonia gas concentration meter,
Outputs deviation signal.

同偏差信号を入力した高低信号選択器は上限又は下限設
定値を越えた偏差信号を選択し、積分調節器へ信号を出
力する。同積分調節器は上記信号を入力し、上記偏差信
号が上限又は下限設定値を越えた時間に比例した転化率
補正信号を出力し、同転化率補正信号は演算器に入力さ
れすると共に、上記転化率補正信号によって補正し、制
御装置が適正なアンモニアガス注入量信号を出力する。
The high/low signal selector inputting the same deviation signal selects the deviation signal exceeding the upper limit or lower limit set value and outputs the signal to the integral controller. The integral regulator inputs the above signal and outputs a conversion rate correction signal proportional to the time when the deviation signal exceeds the upper limit or lower limit set value, and the conversion rate correction signal is input to the arithmetic unit. The control device outputs an appropriate ammonia gas injection amount signal by correcting the conversion rate correction signal.

上記によシ、比較的変化の早い通常のS Os濃度変化
に対応した制御とは別に、転化率補正信号を演算器に入
力することによって経時的なSowよprosへの転化
率のゆるやかな増大に対する制御が行えるようになった
ため、余剰アンモニアガス量を最小限に抑えてアンモニ
アガス注入が行える制御装置が実現できた。
According to the above, in addition to the control that corresponds to normal S Os concentration changes that change relatively quickly, the conversion rate of Sow to Pros can be gradually increased over time by inputting a conversion rate correction signal to the calculator. As a result, a control device that can inject ammonia gas while minimizing the amount of surplus ammonia gas has been realized.

〔実施例〕〔Example〕

本発明の一実施例を第1図に示す。 An embodiment of the present invention is shown in FIG.

本実施例においては、比較器から信号がフィードバック
される部分以外は、従来の装置と同様のため説明を省略
する。
In this embodiment, the parts other than the part where the signal is fed back from the comparator are the same as the conventional device, so the explanation will be omitted.

第1図に示す本実施例は、アンモニアガス濃度設定器1
13が出力した余剰アンモニアガス濃度設定値信号3と
アンモニアガス濃度計111が出力し九アンモニアガス
濃度信号2を入力し偏差信号4を出力する比較器115
、上記偏差信号4を高低信号選択器5を介して入力し転
化率補正信号8を出力する積分調節器7、反応用アンモ
ニアガス量演算回路112よシ出力され九反応用アンモ
ニアガス量信号lを入力し更に燃料中の硫黄分設定値信
号120と上記転化率補正信号8を入力して補正された
反応用アンモニアガス量信号9を出力する演算器6、余
剰用アンモニアガス量演算回路114よシ出力された余
剰用アンモニアガス量信号10を入力し上記余剰アンモ
ニアガス濃度設定値信号3により補正された余剰用アン
モニアガス量信号15を出力する演算器11、上記補正
された反応′用アンモニアガス量信号9と上記余剰用ア
ンモニアガス量信号15を入力して加算しアンモニア量
信号13を出力する加減算器12、上記偏差信号4を入
力した比例積分調節器16が出力した補正用アンモニア
ガス量信号17を入力し補正用余剰アンモニアガス量信
号19を出力する高低設定器18、および上記アンモニ
ア量信号13と補正用余剰アンモニア量信号19を入力
してアンモニア注入量信号を出力する加減算器14を備
えている。
In this embodiment shown in FIG. 1, an ammonia gas concentration setting device 1
A comparator 115 which inputs the surplus ammonia gas concentration setting value signal 3 outputted by 13 and the 9 ammonia gas concentration signal 2 outputted by the ammonia gas concentration meter 111, and outputs a deviation signal 4.
, an integral regulator 7 which inputs the deviation signal 4 through a high/low signal selector 5 and outputs a conversion rate correction signal 8, and a reaction ammonia gas amount calculation circuit 112 outputs a reaction ammonia gas amount signal l. A calculator 6 inputs the fuel sulfur content set value signal 120 and the conversion rate correction signal 8 and outputs a corrected reaction ammonia gas amount signal 9, and a surplus ammonia gas amount calculation circuit 114. A computing unit 11 which inputs the outputted surplus ammonia gas amount signal 10 and outputs a surplus ammonia gas amount signal 15 corrected by the surplus ammonia gas concentration setting value signal 3; An adder/subtractor 12 that inputs and adds the signal 9 and the surplus ammonia gas amount signal 15 and outputs the ammonia amount signal 13, and a correction ammonia gas amount signal 17 outputted by the proportional integral regulator 16 that inputs the deviation signal 4. and an adder/subtractor 14 that inputs the ammonia amount signal 13 and the surplus ammonia gas amount signal 19 for correction and outputs an ammonia injection amount signal. There is.

上記において、比較器115から出力された余剰アンモ
ニアガス設定値信号3とアンモニアガス濃度計信号2の
偏差信号4は高低信号選択1、器5に入力される。同高
低信号選択器5は、上記偏差信号4が同選択器5に設定
された上限値又は下限値を越えた場合に信号を積分調節
器7へ出力し、同調節器7は上記上限値又は下限値を越
え走時間に比例した転化率補正信号8を出力する。同転
化率補正信号8は、反応用アンモニアガス量信号1と硫
黄分設定値信号120を入力した演算器6に入力され、
同演算器6は補正された反応用アンモニアガス量信号9
を出力する。
In the above, the deviation signal 4 between the surplus ammonia gas set value signal 3 outputted from the comparator 115 and the ammonia gas concentration meter signal 2 is input to the high/low signal selection 1 and the device 5. The same high/low signal selector 5 outputs a signal to the integral regulator 7 when the deviation signal 4 exceeds the upper limit or the lower limit set in the selector 5, and the regulator 7 outputs the signal to the above upper limit or lower limit. When the lower limit value is exceeded, a conversion rate correction signal 8 proportional to the running time is output. The conversion rate correction signal 8 is input to the calculator 6 which has input the reaction ammonia gas amount signal 1 and the sulfur content setting value signal 120.
The calculator 6 outputs a corrected reaction ammonia gas amount signal 9.
Output.

上記高低信号選択器5においては、偏差信号が上限値又
は下限値を越えた場合に信号を積分調節器7へ送シ、同
調節器7は上記偏差信号が上限値又は下限値を越えた時
間に比例した転化率補正信号8を出力しているため、通
常の排ガス中のアンモニアガス濃度の変化には応答せず
、経時的なゆるやかな変化が一定の値を越えた段階では
じめて補正が行われる。
In the high/low signal selector 5, when the deviation signal exceeds the upper limit value or the lower limit value, the signal is sent to the integral controller 7, and the regulator 7 sends the signal to the integral controller 7 for the time when the deviation signal exceeds the upper limit value or the lower limit value. Since the conversion rate correction signal 8 is outputted in proportion to be exposed.

上記演算器6よシ出力された補正された反応用アンモニ
アガス量信号1aは、余剰用アンモニアガス量演算回路
114が出力し演算器11によって補正さすした余剰用
アンモニアガス量信号15が加減算器12によって加算
され、同加減算器12はアンモニア量信号13を出力し
加減算器14に入力する。
The corrected reaction ammonia gas amount signal 1a outputted from the arithmetic unit 6 is outputted by the surplus ammonia gas amount calculation circuit 114 and corrected by the arithmetic unit 11. The adder/subtracter 12 outputs an ammonia amount signal 13 and inputs it to the adder/subtracter 14.

また、上記比較器115が出力した偏差信号4は比例積
分調節器16に入力され、同調節器16は通常比較的変
化の早いS Osの濃度変化に対応した補正用アンモニ
アガス量信号17を出力する。同補正用アンモニアガス
量信号17は高低設定器18に入力される。同高低設定
器18は、上記アンモニア濃度計111の応答遅れによ
る極端なアンモニア注入量の過多不足を生じないように
、上記補正用アンモニアガス量信号17に制限を加えた
補正用余剰アンモニアガス量信号19を出力する。
Further, the deviation signal 4 outputted by the comparator 115 is input to the proportional-integral regulator 16, and the regulator 16 outputs a correction ammonia gas amount signal 17 corresponding to the change in the concentration of S Os, which usually changes relatively quickly. do. The correction ammonia gas amount signal 17 is input to the height setting device 18. The height/low setting device 18 generates a surplus ammonia gas amount signal for correction, which is obtained by adding a limit to the ammonia gas amount signal 17 for correction, in order to prevent excessive or insufficient amount of ammonia injection due to the response delay of the ammonia concentration meter 111. Outputs 19.

上記補正用余剰アンモニアガス量信号19は上記加減算
器14に入力され、同加減算器14は上記補正用余剰ア
ンモニアガス量信号19により上記アンモニア量信号1
3を補正し、アンモニア注入量信号20を出力する。
The surplus ammonia gas amount signal 19 for correction is input to the adder/subtractor 14, and the adder/subtractor 14 receives the ammonia amount signal 1 based on the surplus ammonia gas amount signal 19 for correction.
3 is corrected, and an ammonia injection amount signal 20 is output.

上記によシ、経時的なSOlよりS Osへの転化率の
ゆるやかな増大に対する制御と比較的変化の早い通常の
S Osの濃度変化に対応し念制御とがそれぞれ行える
ようになったため、余剰゛アンモニアガス量を最小限に
抑えてアンモニアガス注入が行える制御装置が実現でき
た。
In addition to the above, it has become possible to perform control over the gradual increase in the conversion rate from SOl to SOs over time, and mental control in response to changes in the concentration of normal SOs, which change relatively quickly. ``We have achieved a control device that can inject ammonia gas while minimizing the amount of ammonia gas.

〔発明の効果〕〔Effect of the invention〕

本発明は、反応用アンモニアガス量信号が硫黄分設定値
信号によって補正される演算器を備えアンモニア注入量
信号を出力する制御装置において、余剰アンモニアガス
濃度設定値信号とアンモニア濃度信号を入力する比較器
より偏差信号を高低信号選択器を介して入力し上記演算
器に入力される転化率補正信号を出力する積分調節器を
備えたことによって、比較的変化の早い通常のS Os
濃度変化に対応した制御とは別に、転化率補正信号を演
算器に入力することによって経時的なSOlより so
sへの転化率のゆるやかな増大に対する制御が行えるよ
うになったため、余剰アンモニアガス量を最小限に抑え
てアンモニアガス注入が行える制御装置が実現できた。
The present invention provides a control device that outputs an ammonia injection amount signal and is equipped with an arithmetic unit in which a reaction ammonia gas amount signal is corrected by a sulfur content setting value signal, and a comparison device that inputs an excess ammonia gas concentration setting value signal and an ammonia concentration signal. By providing an integral regulator that inputs a deviation signal from the converter via a high/low signal selector and outputs a conversion rate correction signal that is input to the above-mentioned arithmetic unit, the normal SO
In addition to the control corresponding to concentration changes, by inputting a conversion rate correction signal to a calculator, SOl can be improved over time.
Since it has become possible to control the gradual increase in the conversion rate to s, a control device that can inject ammonia gas while minimizing the amount of surplus ammonia gas has been realized.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例の説明図、第2図はアンモニ
アガス注入脱硫装置の説明図、第3図は従来の装置の説
明図である。 1・・・反応用アンモニアガス量信号、2・・・アンモ
ニアガス濃度信号、3・・・余剰アンモニアガス濃度設
定値信号、4・・・偏差信号、5・・・高低信号選択器
、6・・・演算器、7・・・積分調節器、8・・・転化
率補正信号、9・・−反応用アンモニアガス量信号、1
0・・・余剰用アンモニアガス量信号、11・・・演算
器、12・・・加減算器、13・・・アンモニア量信号
、14・・・加減算器、15・・・余剰用アンモニアガ
ス量信号、16・・・比例積分調節器、17・・・補正
用アンモニアガス量信号、18・・・高低設定器、19
・・・補正用余剰アンモニアガス量信号、20・・・ア
ンモニアガス注入量信号、101・・・燃料流量信号、
111・・・アンモニアガス濃度計、112・・・反応
用アンモニアガス量信号、113・・・アンモニアガス
濃度設定!、114・・・余剰用アンモニアガス量演算
回路、115・・・比較器。 代理人 弁理士  坂 間    暁     外2名
躬1色 fi2m 肩3rA
FIG. 1 is an explanatory diagram of an embodiment of the present invention, FIG. 2 is an explanatory diagram of an ammonia gas injection desulfurization apparatus, and FIG. 3 is an explanatory diagram of a conventional apparatus. DESCRIPTION OF SYMBOLS 1... Reaction ammonia gas amount signal, 2... Ammonia gas concentration signal, 3... Excess ammonia gas concentration setting value signal, 4... Deviation signal, 5... High/low signal selector, 6... ... Arithmetic unit, 7... Integral controller, 8... Conversion rate correction signal, 9...-Ammonia gas amount signal for reaction, 1
0... Surplus ammonia gas amount signal, 11... Arithmetic unit, 12... Addition/subtraction device, 13... Ammonia amount signal, 14... Addition/subtraction device, 15... Surplus ammonia gas amount signal , 16... Proportional integral adjuster, 17... Ammonia gas amount signal for correction, 18... Height setting device, 19
... Surplus ammonia gas amount signal for correction, 20... Ammonia gas injection amount signal, 101... Fuel flow rate signal,
111...Ammonia gas concentration meter, 112...Ammonia gas amount signal for reaction, 113...Ammonia gas concentration setting! , 114... Surplus ammonia gas amount calculation circuit, 115... Comparator. Agent Patent Attorney Akatsuki Sakama 2 people 1 color fi 2m shoulder 3rA

Claims (1)

【特許請求の範囲】[Claims] 反応用アンモニアガス量信号を燃料中の硫黄分設定値信
号によつて補正する演算器を備えアンモニア注入量信号
を出力する制御装置において、アンモニアガス濃度設定
器が出力する余剰アンモニアガス濃度設定値信号とアン
モニアガス濃度計が出力するアンモニアガス濃度信号を
入力する比較器、同比較器が出力する偏差信号を入力し
上限又は下限設定値を越えた偏差信号を選択する高低信
号選択器、同高低信号選択器が出力した信号を入力し上
記偏差信号が上限又は下限設定値を越えた時間に比例し
た転化率補正信号を出力し同信号を上記演算器に入力さ
せる積分調節器を備えたことを特徴とするアンモニアガ
ス注入量の制御装置。
In a control device that outputs an ammonia injection amount signal and is equipped with a calculation unit that corrects a reaction ammonia gas amount signal based on a sulfur content set value signal in the fuel, the surplus ammonia gas concentration set value signal outputted by the ammonia gas concentration setting device. A comparator that inputs the ammonia gas concentration signal output by the ammonia gas concentration meter, a high/low signal selector that inputs the deviation signal output from the comparator and selects the deviation signal that exceeds the upper or lower limit set value, and the same high/low signal. It is characterized by comprising an integral controller which inputs the signal output from the selector, outputs a conversion rate correction signal proportional to the time when the deviation signal exceeds the upper limit or lower limit set value, and inputs the signal to the arithmetic unit. A control device for the amount of ammonia gas injected.
JP1035023A 1989-02-16 1989-02-16 Control device for ammonia gas injection volume Expired - Lifetime JP2695654B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1035023A JP2695654B2 (en) 1989-02-16 1989-02-16 Control device for ammonia gas injection volume

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1035023A JP2695654B2 (en) 1989-02-16 1989-02-16 Control device for ammonia gas injection volume

Publications (2)

Publication Number Publication Date
JPH02214521A true JPH02214521A (en) 1990-08-27
JP2695654B2 JP2695654B2 (en) 1998-01-14

Family

ID=12430460

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1035023A Expired - Lifetime JP2695654B2 (en) 1989-02-16 1989-02-16 Control device for ammonia gas injection volume

Country Status (1)

Country Link
JP (1) JP2695654B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015136867A1 (en) * 2014-03-14 2015-09-17 川崎重工業株式会社 Scrubber and engine system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015136867A1 (en) * 2014-03-14 2015-09-17 川崎重工業株式会社 Scrubber and engine system

Also Published As

Publication number Publication date
JP2695654B2 (en) 1998-01-14

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